US7211346B2 - Corrosion resistant metallic bipolar plate - Google Patents
Corrosion resistant metallic bipolar plate Download PDFInfo
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- US7211346B2 US7211346B2 US10/403,472 US40347203A US7211346B2 US 7211346 B2 US7211346 B2 US 7211346B2 US 40347203 A US40347203 A US 40347203A US 7211346 B2 US7211346 B2 US 7211346B2
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/24—Nitriding
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C19/00—Alloys based on nickel or cobalt
- C22C19/03—Alloys based on nickel or cobalt based on nickel
- C22C19/05—Alloys based on nickel or cobalt based on nickel with chromium
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C30/00—Coating with metallic material characterised only by the composition of the metallic material, i.e. not characterised by the coating process
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/24—Nitriding
- C23C8/26—Nitriding of ferrous surfaces
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to components such as metal bipolar plates for proton exchange membrane (PEM) fuel cells and other chemical-to-electrical energy conversion devices, and more particularly to metal bipolar plates having thermally grown nitrided surface layers to enhance corrosion resistance thereof.
- PEM proton exchange membrane
- Chemical-to-electrical energy conversion devices are of great interest as efficient, non-polluting power sources for automotive applications, and also for stationary applications such as distributed power sources for buildings and houses as well as portable power generation for consumer electronic devices.
- a major barrier to commercial application of this technology is the cost of the devices.
- bipolar plate serves to separate fuel and oxidant and to connect the cathode of one cell to the anode of the adjacent cell in a stacked series.
- the cost of the machined graphite bipolar plates in PEM fuel cells accounts for as much as 60% of the overall fuel cell stack costs.
- Metallic bipolar plates offer the potential for significantly lower cost since they can be formed by readily available and inexpensive conventional metal forming processes.
- a well-known drawback of metallic bipolar plates is that they generally exhibit inadequate corrosion resistance, which leads to high electrical resistance and/or PEM contamination, degrading fuel cell performance to unacceptable levels.
- Corrosion-resistant coatings have been applied to metallic bipolar plates, but surface defects therein have limited the success thereof.
- objects of the present invention include the provision of: metal bipolar plates and other metallic components having enhanced corrosion resistance without sacrificing electrical conductance thereof; efficient and low cost PEM fuel cells that last longer in corrosive environments, and improved power generation. Further and other objects of the present invention will become apparent from the description contained herein.
- a corrosion resistant, electrically conductive component which includes 20–55% Cr, balance base metal.
- the component has thereon a substantially external, continuous layer of chromium nitride.
- a proton exchange membrane fuel cell includes a corrosion resistant, electrically conductive bipolar plate.
- the bipolar plate includes 20–55% Cr, balance base metal.
- the component has thereon a substantially external, continuous layer of chromium nitride.
- FIG. 1 is a graph showing anodic polarization curves for binary bipolar plate material made in accordance with the present invention compared with other materials.
- FIG. 2 is a scanning electron photomicrograph showing a cross-section of Ni-50Cr (Cr 50%, balance Ni) nitrided at 1100° C. for 1 hr. in N 2 in accordance with the present invention.
- FIG. 3 is a graph showing anodic polarization curves for ternary bipolar plate materials made in accordance with the present invention.
- Bipolar plate and other components made with base metal-Cr substrates have a distinct advantage in forming a nitride or carbonitride layer for corrosion protection. As the nitride or carbonitride layer is grown, three distinct, beneficial, and unexpected advantages are manifest:
- the present invention provides an essentially uniform, defect-free, external layer of material that is both corrosion resistant and amenable to the function of the component. Chromium nitrides and carbonitrides are also highly electrically conductive.
- a key feature is the formation of an external, continuous, dense, surface nitride layer of Cr 2 N and/or CrN.
- a continuous or discontinuous outer layer of CrN may form over an inner Cr 2 N layer.
- Cr 2 N appears to have better overall corrosion resistance, but CrN may also be beneficial under some corrosion conditions, especially when present as an outer continuous layer.
- the base alloy composition, microstructure, and nitridation process conditions should be selected and controlled in order to avoid, as much as possible:
- Some embodiments of the invention employ a binary alloy comprising 20–55% Cr, balance Ni, preferably 30–53% Cr, balance Ni, more preferably 40–52% Cr, balance Ni, most preferably 45–51% Cr, balance Ni. Too little Cr will result in formation of an insufficient amount of Cr 2 N to produce a continuous layer thereof. Too much Cr will result in a composition that work-hardens too quickly and is difficult to deform mechanically into the desired shape. The amount of Cr is desirably minimized due to higher cost thereof.
- Base metal is defined, for the purposes of describing the present invention, as any metal or alloy that is compatible with Cr.
- Ni is shown herein to be a particularly good base metal
- ternary Fe(Ni)—Cr or Ni(Fe)—Cr alloys (ferritic and/or austenitic) with Cr levels in the ranges set forth hereinabove are also expected to exhibit external Cr-nitride layer (also referred to as scale) formation and corresponding excellent corrosion resistance in accordance with the present invention.
- Base metals Ni, Ni(Fe), Fe(Ni), and Fe and alloys are preferred.
- Fe-based alloys can contain 5–25%Ni
- Ni-based alloys can contain 5–25% Fe.
- Other alloy bases, notably Co, or cladding of these base metals onto less expensive substrates e.g. Cu, Al, Fe, or stainless steels
- Alloying additions of other elements are useful to decrease the permeability of nitrogen in the component, and to reduce the level of Cr and/or Ni and/or Fe in the alloy needed to form the desired external Cr nitride layer. Reduction in Cr and Ni is favored to reduce cost and/or improve manufacturability.
- alloying additions include, but are not limited to, at least one of Co, Cu, Fe, Mn, and Mo. Ni addition to Fe base alloys is also similarly beneficial. Such alloying additions are generally in the range of 3–20%, but can be more or less, depending on the specific composition of the component.
- Additions of reactive elements and/or rare earth elements can be used to modify the growth of the nitride layer to make it more inward growing and adherent. Additions of Hf and Zr are particularly favored due to their great stability with nitrogen and solubility in Ni. Additions of Y, La, Ce, and combinations thereof such as in misch metal are also suggested. Additions of reactive elements and/or rare earth elements are generally in the range of up to 1%, preferably 0.05–0.5%.
- Alloying additions to modify the Cr-nitride may also be effective to further improve stability/corrosion resistance.
- These include refractory and transition metal elements of greater stability with nitrogen than Cr, particularly Nb, Ti, V, and Zr.
- Such alloying additions are generally in the range of up to 10%, with preferable ranges of up to 3% for Zr, Ti and 3–7% for Nb, V.
- Thermal nitridation and/or carbonitridation are carried out according to well-known methods.
- resultant nitrogen levels in the range of 1–5 mg/cm 2 are the general target with levels in the range of 2–3 mg/cm 2 being preferred to minimize the chances for scale spallation or cracking.
- Nitridation was generally conducted at a temperature in the range of 800° C. to 1200° C. in pure nitrogen or 96% nitrogen-4% hydrogen mixtures, although a temperature as low as 400° C. in ammonia environments is also suitable.
- the alloys can also be nitrided in a graphite furnace to introduce carbon into the nitride layer, which can further increase corrosion resistance. Carburization, carbonitridation, and boronization are also expected to produce similar corrosion resistant layers.
- the surface treatment can also be accomplished by plasma assisted and related processes well established in the art, which permit lower temperature nitridation.
- External nitride formation can also be favored by use of a gaseous atmosphere with a reduced nitrogen partial pressure. Such conditions are well known to favor external nitridation reactions over discontinuous internal nitridation due to the corresponding decrease in alloy nitrogen solubility and inward nitrogen flux. Such a method can also be used to eliminate formation of less stable base metal nitrides.
- External Cr-nitride formation can also be accomplished by first forming a Cr oxide layer, which enriches the surface with Cr, and subsequently converting the Cr-oxide to Cr-nitride by a nitridation method particularly using ammonia or other nitrogen hydrogen mixtures. This is particularly beneficial because the critical Cr concentration to form an external layer is much lower for oxidation than nitridation in most alloys.
- An alloy of composition Ni-50Cr was arc-cast and then heat-treated at 1100° C. for 8 h in vacuum. Alloy coupons were cut and abraded to a 240–600 grit surface finish. Nitridation of the coupons was carried out by heating in nitrogen at a temperature of 1100° C. for various periods of time: 1, 2, and 3 hours. The coupons treated for 2 hours resulted in 2 mg/cm 2 nitrogen. Corrosion resistance performance thereof was tested and compared to other materials by exposure to aerated pH 3 sulfuric acid at a temperature of 80° C. Results of the tests are shown in FIG. 1 .
- FIG. 1 shows anodic polarization curves (scan rate 0.1 mV/sec) for various bipolar plate materials tested in Example I.
- Curve 1 is for nitrided Ni-50Cr prepared as described above in Example I.
- Curve 2 is for non-nitrided Ni-50Cr.
- Curve 3 is for commercial purity Ti.
- Curve 4 is for commercial purity Ni. Data show that corrosion resistance performance of material made in accordance with the present invention is significantly better than for other tested materials.
- FIG. 2 shows the microstructure of a cross-section of Ni-50Cr with its surface nitrided as described above in Example I. Four distinct regions are visible: base material 1 comprised of Ni-50Cr; ternary ⁇ Ni—Cr—N phase 2 , which is not significantly corrosion resistant; a continuous external Cr 2 N surface layer 3 , which is the key source of corrosion protection for the alloy; and an overlying, discontinuous CrN phase 4 .
- Ni-42Cr base alloys were modified with Mo, Mn, Fe additions and nitrided as described in Example I. Corrosion resistance performance thereof was tested as described in Example I. Results are shown in FIG. 3 , which shows anodic polarization curves (scan rate 0.1 mV/sec) for three modified Ni-42Cr base alloys as follows:
- the bipolar plate materials of the present invention are also applicable to direct methanol fuel cell, battery, and other low temperature ( ⁇ 200–300° C. operation) fuel cell (e.g. phosphoric acid fuel cell) and electrochemical-based power generation devices where metallic components requiring a combination of electrical conductivity and corrosion resistance are needed.
- fuel cell e.g. phosphoric acid fuel cell
- electrochemical-based power generation devices where metallic components requiring a combination of electrical conductivity and corrosion resistance are needed.
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Abstract
Description
-
- 1. Chromium nitrides and/or carbonitrides are formed preferentially over base metal nitrides and/or carbonitrides. The advantage is that chromium nitrides and carbonitrides are corrosion resistant, while the presence of base metal nitrides and carbonitrides would generally degrade corrosion resistance.
- 2. Chromium nitrides and/or carbonitrides are formed preferentially on the surface of the component rather than internally. The advantage is that corrosion resistance is needed at the surface. Internally formed corrosion resistant materials are not useful in that they leave the component surface exposed to corrosive environments.
- 3. Chromium nitrides and/or carbonitrides are formed with few or no defects that would allow corrosive materials to attack the component material therethrough.
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- 1. Deleterious defects such as discontinuous surface Cr2N and/or introduction of substantial amounts of base metal such as Fe or Ni (more than 0.5–1%) into the nitride surface layer.
- 2. Formation of mixed ternary and higher-order Cr-nitrides with the base metal at the surface, for example, Cr—Fe—N and/or Ni—Cr—N phases.
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- 1. Nitrided Ni-42Cr-5Mn, 2.8 mg/cm2N
- 2. Nitrided Ni-42Cr-5Mo, 1.6 mg/cm2N
- 3. Nitrided Ni-42Cr-10Fe, 2.0 mg/cm2N
Claims (18)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US10/403,472 US7211346B2 (en) | 2002-04-03 | 2003-03-31 | Corrosion resistant metallic bipolar plate |
US11/582,034 US7829194B2 (en) | 2003-03-31 | 2006-10-17 | Iron-based alloy and nitridation treatment for PEM fuel cell bipolar plates |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US36975402P | 2002-04-03 | 2002-04-03 | |
US10/403,472 US7211346B2 (en) | 2002-04-03 | 2003-03-31 | Corrosion resistant metallic bipolar plate |
Related Child Applications (1)
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US11/582,034 Continuation-In-Part US7829194B2 (en) | 2003-03-31 | 2006-10-17 | Iron-based alloy and nitridation treatment for PEM fuel cell bipolar plates |
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US20030190515A1 US20030190515A1 (en) | 2003-10-09 |
US7211346B2 true US7211346B2 (en) | 2007-05-01 |
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Cited By (2)
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US20090286107A1 (en) * | 2008-05-13 | 2009-11-19 | Ut-Battelle, Llc | Ferritic Alloy Compositions |
US10511030B2 (en) | 2016-11-28 | 2019-12-17 | Industrial Technology Research Institute | Anti-corrosion structure and fuel cell employing the same |
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US7829194B2 (en) * | 2003-03-31 | 2010-11-09 | Ut-Battelle, Llc | Iron-based alloy and nitridation treatment for PEM fuel cell bipolar plates |
JP2006134855A (en) * | 2004-03-11 | 2006-05-25 | Nissan Motor Co Ltd | Separator for fuel cell, fuel cell stack, fuel cell vehicle, and manufacturing method of separator for fuel cell |
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US7247403B2 (en) * | 2004-04-21 | 2007-07-24 | Ut-Battelle, Llc | Surface modified stainless steels for PEM fuel cell bipolar plates |
US7309540B2 (en) * | 2004-05-21 | 2007-12-18 | Sarnoff Corporation | Electrical power source designs and components |
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US20110262831A1 (en) * | 2010-04-22 | 2011-10-27 | Gm Global Technlogy Operations, Inc. | Formed plate assembly for pem fuel cell |
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US10003089B2 (en) | 2015-02-11 | 2018-06-19 | Ford Global Technologies, Llc | Multilayer coating for corrosion resistant metal bipolar plate for a PEMFC |
US10135077B2 (en) * | 2015-02-12 | 2018-11-20 | Ford Global Technologies, Llc | Corrosion resistant metal bipolar plate for a PEMFC including a radical scavenger |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3841847A (en) * | 1972-09-15 | 1974-10-15 | British Non Ferrous Metals Res | Chromium alloys containing y{11 o{11 {11 and aluminium or silicon or both |
US5445683A (en) * | 1992-05-13 | 1995-08-29 | Daidousanso Co., Ltd. | Nickel alloy products with their surfaces nitrided and hardened |
US5683828A (en) | 1994-10-12 | 1997-11-04 | H Power Corp. | Metal platelet fuel cells production and operation methods |
US5798188A (en) | 1997-06-25 | 1998-08-25 | E. I. Dupont De Nemours And Company | Polymer electrolyte membrane fuel cell with bipolar plate having molded polymer projections |
US20010039984A1 (en) * | 2000-04-11 | 2001-11-15 | Toshiaki Nonomura | Manufacturing process of nickel-based alloy having improved hot sulfidation-corrosion resistance |
US20020057984A1 (en) * | 2000-09-14 | 2002-05-16 | Bohler Edelstahl Gmbh | Nickel-based alloy for high-temperature technology |
US20020081478A1 (en) * | 2000-11-24 | 2002-06-27 | Ilona Busenbender | Bipolar plate |
-
2003
- 2003-03-31 US US10/403,472 patent/US7211346B2/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3841847A (en) * | 1972-09-15 | 1974-10-15 | British Non Ferrous Metals Res | Chromium alloys containing y{11 o{11 {11 and aluminium or silicon or both |
US5445683A (en) * | 1992-05-13 | 1995-08-29 | Daidousanso Co., Ltd. | Nickel alloy products with their surfaces nitrided and hardened |
US5683828A (en) | 1994-10-12 | 1997-11-04 | H Power Corp. | Metal platelet fuel cells production and operation methods |
US5798188A (en) | 1997-06-25 | 1998-08-25 | E. I. Dupont De Nemours And Company | Polymer electrolyte membrane fuel cell with bipolar plate having molded polymer projections |
US20010039984A1 (en) * | 2000-04-11 | 2001-11-15 | Toshiaki Nonomura | Manufacturing process of nickel-based alloy having improved hot sulfidation-corrosion resistance |
US20020057984A1 (en) * | 2000-09-14 | 2002-05-16 | Bohler Edelstahl Gmbh | Nickel-based alloy for high-temperature technology |
US20020081478A1 (en) * | 2000-11-24 | 2002-06-27 | Ilona Busenbender | Bipolar plate |
Non-Patent Citations (3)
Title |
---|
A. A. Kodentsov et al, "High-Temperature Nitridation of Ni-Cr Alloys," Metallurgical & Materials Transactions A, vol. 27A, (Jan. 1996) pp. 59-69. |
G. Bertrand et al, "A Study of the Corrosion Behaviour and Protective Quality of Sputtered Chromium Nitride Coatings," Surface and Coatings Technology 126 (2000) 199-209, Elsevier. |
Masami Taguchi et al, "Effect of Surface Nitriding on Corrosion Resistance of Chromium in Sulfuric Acid Solution," Materials Transactions, KIM, vol. 32, #12 (1991), pp. 1170-1176. |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090286107A1 (en) * | 2008-05-13 | 2009-11-19 | Ut-Battelle, Llc | Ferritic Alloy Compositions |
US10511030B2 (en) | 2016-11-28 | 2019-12-17 | Industrial Technology Research Institute | Anti-corrosion structure and fuel cell employing the same |
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US20030190515A1 (en) | 2003-10-09 |
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